SK112094A3 - Method of vitamin d producing - Google Patents
Method of vitamin d producing Download PDFInfo
- Publication number
- SK112094A3 SK112094A3 SK1120-94A SK112094A SK112094A3 SK 112094 A3 SK112094 A3 SK 112094A3 SK 112094 A SK112094 A SK 112094A SK 112094 A3 SK112094 A3 SK 112094A3
- Authority
- SK
- Slovakia
- Prior art keywords
- acid
- reaction
- mixture
- tocopherol
- trimethylhydroquinone
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 14
- 229940046008 vitamin d Drugs 0.000 title 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000000203 mixture Substances 0.000 claims abstract description 28
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 claims abstract description 27
- GVJHHUAWPYXKBD-UHFFFAOYSA-N d-alpha-tocopherol Natural products OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- AUFZRCJENRSRLY-UHFFFAOYSA-N 2,3,5-trimethylhydroquinone Chemical compound CC1=CC(O)=C(C)C(C)=C1O AUFZRCJENRSRLY-UHFFFAOYSA-N 0.000 claims abstract description 17
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims abstract description 16
- 235000010338 boric acid Nutrition 0.000 claims abstract description 16
- 229960002645 boric acid Drugs 0.000 claims abstract description 16
- 235000006408 oxalic acid Nutrition 0.000 claims abstract description 14
- 239000011732 tocopherol Substances 0.000 claims abstract description 13
- 229960001295 tocopherol Drugs 0.000 claims abstract description 13
- 239000002904 solvent Substances 0.000 claims abstract description 12
- GVJHHUAWPYXKBD-IEOSBIPESA-N α-tocopherol Chemical compound OC1=C(C)C(C)=C2O[C@@](CCC[C@H](C)CCC[C@H](C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-IEOSBIPESA-N 0.000 claims abstract description 12
- ZAKOWWREFLAJOT-UHFFFAOYSA-N DL-alpha-tocopherylacetate Chemical compound CC(=O)OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C ZAKOWWREFLAJOT-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229930003799 tocopherol Natural products 0.000 claims abstract description 11
- 235000010384 tocopherol Nutrition 0.000 claims abstract description 11
- 239000001707 (E,7R,11R)-3,7,11,15-tetramethylhexadec-2-en-1-ol Substances 0.000 claims abstract description 10
- BLUHKGOSFDHHGX-UHFFFAOYSA-N Phytol Natural products CC(C)CCCC(C)CCCC(C)CCCC(C)C=CO BLUHKGOSFDHHGX-UHFFFAOYSA-N 0.000 claims abstract description 10
- HNZBNQYXWOLKBA-UHFFFAOYSA-N Tetrahydrofarnesol Natural products CC(C)CCCC(C)CCCC(C)=CCO HNZBNQYXWOLKBA-UHFFFAOYSA-N 0.000 claims abstract description 10
- BOTWFXYSPFMFNR-OALUTQOASA-N all-rac-phytol Natural products CC(C)CCC[C@H](C)CCC[C@H](C)CCCC(C)=CCO BOTWFXYSPFMFNR-OALUTQOASA-N 0.000 claims abstract description 10
- BOTWFXYSPFMFNR-PYDDKJGSSA-N phytol Chemical compound CC(C)CCC[C@@H](C)CCC[C@@H](C)CCC\C(C)=C\CO BOTWFXYSPFMFNR-PYDDKJGSSA-N 0.000 claims abstract description 10
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 5
- 230000032050 esterification Effects 0.000 claims abstract description 3
- 238000005886 esterification reaction Methods 0.000 claims abstract description 3
- 235000001809 DL-alpha-tocopherylacetate Nutrition 0.000 claims abstract 3
- 239000011626 DL-alpha-tocopherylacetate Substances 0.000 claims abstract 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 18
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 claims description 7
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 claims description 7
- 239000011975 tartaric acid Substances 0.000 claims description 7
- 235000002906 tartaric acid Nutrition 0.000 claims description 7
- 235000015165 citric acid Nutrition 0.000 claims description 6
- -1 on the one hand Chemical compound 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 5
- 229940087168 alpha tocopherol Drugs 0.000 claims 2
- 229960000984 tocofersolan Drugs 0.000 claims 2
- 239000002076 α-tocopherol Substances 0.000 claims 2
- KEVYVLWNCKMXJX-ZCNNSNEGSA-N Isophytol Natural products CC(C)CCC[C@H](C)CCC[C@@H](C)CCC[C@@](C)(O)C=C KEVYVLWNCKMXJX-ZCNNSNEGSA-N 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 150000003628 tricarboxylic acids Chemical class 0.000 abstract description 2
- 125000001931 aliphatic group Chemical group 0.000 abstract 1
- 229940117373 dl-alpha tocopheryl acetate Drugs 0.000 abstract 1
- 229940042585 tocopherol acetate Drugs 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 30
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 16
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 13
- 239000011541 reaction mixture Substances 0.000 description 13
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- ZAKOWWREFLAJOT-CEFNRUSXSA-N D-alpha-tocopherylacetate Chemical compound CC(=O)OC1=C(C)C(C)=C2O[C@@](CCC[C@H](C)CCC[C@H](C)CCCC(C)C)(C)CCC2=C1C ZAKOWWREFLAJOT-CEFNRUSXSA-N 0.000 description 10
- FDPIMTJIUBPUKL-UHFFFAOYSA-N pentan-3-one Chemical compound CCC(=O)CC FDPIMTJIUBPUKL-UHFFFAOYSA-N 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 239000000243 solution Substances 0.000 description 8
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 8
- 239000003054 catalyst Substances 0.000 description 7
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 229930003427 Vitamin E Natural products 0.000 description 6
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 6
- 235000011167 hydrochloric acid Nutrition 0.000 description 6
- 239000011709 vitamin E Substances 0.000 description 6
- 229940046009 vitamin E Drugs 0.000 description 6
- 235000019165 vitamin E Nutrition 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- FOYKKGHVWRFIBD-UHFFFAOYSA-N gamma-tocopherol acetate Natural products CC(=O)OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1 FOYKKGHVWRFIBD-UHFFFAOYSA-N 0.000 description 5
- 238000004817 gas chromatography Methods 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- 238000004508 fractional distillation Methods 0.000 description 4
- 239000011592 zinc chloride Substances 0.000 description 4
- 235000005074 zinc chloride Nutrition 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 3
- 150000002576 ketones Chemical class 0.000 description 3
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 3
- SYBYTAAJFKOIEJ-UHFFFAOYSA-N 3-Methylbutan-2-one Chemical compound CC(C)C(C)=O SYBYTAAJFKOIEJ-UHFFFAOYSA-N 0.000 description 2
- 239000011740 D-alpha-tocopherylacetate Substances 0.000 description 2
- 235000002414 D-alpha-tocopherylacetate Nutrition 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical class FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229940039770 d-alpha-tocopheryl acetate Drugs 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 235000011007 phosphoric acid Nutrition 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- SLYWWALAGATHAB-UHFFFAOYSA-N 2,3,5-triethylbenzene-1,4-diol Chemical compound CCC1=CC(O)=C(CC)C(CC)=C1O SLYWWALAGATHAB-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 229910015900 BF3 Inorganic materials 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- VHGBWHGICRTHIQ-UHFFFAOYSA-N phytadiene Natural products CCCCCCCCCCCCCCCC=C(/C)C=C VHGBWHGICRTHIQ-UHFFFAOYSA-N 0.000 description 1
- 239000002798 polar solvent Substances 0.000 description 1
- 238000002390 rotary evaporation Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- WBHQBSYUUJJSRZ-UHFFFAOYSA-M sodium bisulfate Chemical compound [Na+].OS([O-])(=O)=O WBHQBSYUUJJSRZ-UHFFFAOYSA-M 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L sodium sulphate Substances [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- YNJBWRMUSHSURL-UHFFFAOYSA-N trichloroacetic acid Chemical compound OC(=O)C(Cl)(Cl)Cl YNJBWRMUSHSURL-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D311/00—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
- C07D311/02—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D311/04—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
- C07D311/58—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4
- C07D311/70—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4 with two hydrocarbon radicals attached in position 2 and elements other than carbon and hydrogen in position 6
- C07D311/72—3,4-Dihydro derivatives having in position 2 at least one methyl radical and in position 6 one oxygen atom, e.g. tocopherols
Abstract
Description
Oblasť technikyTechnical field
Tento vynález sa týka zlepšeného spôsobu výroby vitamínu E, kyslo katalyzovanou reakciou 2,3,5-trimetylhydrochinónu (TMH) s fytolom.The present invention relates to an improved process for the production of vitamin E by acid catalyzed reaction of 2,3,5-trimethylhydroquinone (TMH) with phytol.
Doterajší stav technikyBACKGROUND OF THE INVENTION
Je známe, že sa d,1-a-tokoferol (vitamín E) vyrobí reakciouIt is known that d, l-α-tocopherol (vitamin E) is produced by a reaction
2,3,5-trimetylhydrochinónu a fytolu, prípadne izofytolu (IP), pri zvýšenej teplote v málo polárnom rozpúšťadle za prítomnosti rôznych kyslých katalyzátorov.2,3,5-trimethylhydroquinone and phytol or isophytol (IP) at elevated temperature in a low-polar solvent in the presence of various acid catalysts.
Podlá údajov obsiahnutých v Chem. Abstracts (C.A. ) 84 , 59792 /1976/ a Chem. Abstracts 85, 46898 /1976/ sa môže reakcia uskutočňovať za prítomnosti oxidu kremičitého a/alebo oxidu hlinitého s kyselinami.According to the data contained in Chem. Abstracts (C.A.) 84, 59792 (1976) and Chem. Abstracts 85, 46898 (1976), the reaction may be carried out in the presence of silica and / or alumina with acids.
Podlá Chem. Abstracts 73, 77483 /1970/, Chem. Abstracts 80, 3385 /1974/, Chem. Abstracts 80, 3386 /1974/, Chem. Abstracts 73, 98799 /1970/ a DE-OS 22 08 795 sa môže reakcia tiež uskutočňovať za prítomnosti chloridu zinočnatého v kombinácii s kyselinami, ako s halogénovodíkovými kyselinami, predovšetkým s kyselinou chlorovodíkovou alebo kyselinou trichlóroctovou alebo s kyselinou octovou.According to Chem. 73, 77483 (1970), Chem. 80, 3385 (1974), Chem. 80, 3386 (1974), Chem. Abstracts 73, 98799 (1970) and DE-OS 22 08 795, the reaction can also be carried out in the presence of zinc chloride in combination with acids such as hydrohalic acids, in particular hydrochloric or trichloroacetic acid or acetic acid.
Podlá údajov z DE-A 22 08 795 je tiež použitelný chlorid zinočnatý v zmesi s hydrogénsíranom sodným, kyselinou sírovou alebo kyselinou p-toluénsulfónovou, v molárnom pomere od 1:3 do 1:1.According to DE-A 22 08 795, it is also possible to use zinc chloride in a mixture with sodium hydrogen sulphate, sulfuric acid or p-toluenesulphonic acid, in a molar ratio of from 1: 3 to 1: 1.
Podlá informácie obsiahnutej v Chem. Abstracts 84., 74471 /1976/ možno reakciu uskutočniť v perchlóretyléne, za prítomnosti zmesi oxidu kremičitého a oxidu hlinitého v pomere 87:13 ako katalyzátora.According to the information contained in Chem. Abstracts 84, 74471 (1976), can be carried out in perchlorethylene, in the presence of a 87:13 silica / alumina mixture as a catalyst.
Podľa US patentu č. 3 459 773 sa vitamín E získa reakciou fytolu alebo izofytolu s 2,3,5-trimetylhydrochinónom v inertnom rozpúšťadle za použitia makroretikulárnej katiónmeničovej živice typu odvodeného od kyseliny sulfónovej.According to U.S. Pat. No. 3,459,773, vitamin E is obtained by reacting phytol or isophytol with 2,3,5-trimethylhydroquinone in an inert solvent using a macroreticular cation exchange resin of the sulfonic acid type.
Spoločným znakom týchto známych spôsobov je, že nedovoľujú vyrábať vitamín E vo veľkom technickom merítku v požadovanej čistote.A common feature of these known processes is that they do not permit the production of vitamin E on a large scale in the required purity.
Na prekonanie tohto problému bola uskutočnená reakcia podľa DE 27 43 920 za prítomnosti zmesi kyseliny kremičitej a/alebo oxidu hlinitého alebo silikagelu a chloridu zinočnatého, rovnako ako silnej kyseliny, ako koncentrovanej kyseliny chlorovodíkovej, kyseliny sírovej, kyseliny fosforečnej alebo kyseliny p-toluénsulfónovej.To overcome this problem, a reaction according to DE 27 43 920 was carried out in the presence of a mixture of silicic acid and / or alumina or silica gel and zinc chloride, as well as a strong acid such as concentrated hydrochloric acid, sulfuric acid, phosphoric acid or p-toluenesulfonic acid.
Nedostatkom tohto spôsobu rovnako ako u vyššie uvedených spôsobov je, že vznikajú problémy s koróziou a že môže nastať zaťaženie odpadových vôd iónami zinku.The disadvantage of this method, as with the above-mentioned methods, is that corrosion problems arise and that zinc ion loads can occur in the waste water.
Úlohou vynálezu je nájsť katalytický systém pre reakciuThe object of the invention is to find a catalyst system for the reaction
2,3,5-trimetylhydrochinónu s fytolom alebo izofytolom na vitamín E, pomocou ktorého by jednoduchšie prebiehala výroba vitamínu E tiež vo väčšom merítku ako podľa doterajšieho stavu techniky. K tomu je potrebné, aby katalytický systém nebol toxický (ako adukty fluoridu bóritého), aby nemal korózne účinky (ako chlorid zinočnatý, kyselina chlorovodíková, kyselina mravenčia a kyselina fosforečná), aby nežiadúce vedľajšie reakcie, ako dehydratácia izofytolu na fytadién boli čo najviac potlačené a aby reakcie drahých a citlivých východiskových látok boli katalyzované tiež pri nasadení ekvimolárnych množstiev vo vysokých výťažkoch, lebo prebytočné východiskové látky sú oddeliteľné iba s veľkou spotrebou reakčného produktu.2,3,5-trimethylhydroquinone with phytol or isophytol to vitamin E, which would make it easier to produce vitamin E also on a larger scale than in the prior art. To this end, the catalytic system must be non-toxic (such as boron trifluoride adducts), have no corrosive effects (such as zinc chloride, hydrochloric acid, formic acid and phosphoric acid), so that unwanted side reactions such as dehydration of isophytol to phytadiene are suppressed and that the reactions of expensive and sensitive starting materials are catalyzed also when equimolar amounts are used in high yields, since excess starting materials are separable only with a large consumption of the reaction product.
Podstata vynálezuSUMMARY OF THE INVENTION
Nedávno sa zistilo, že zmes kyseliny ortobóritej na strane jednej a určitých dikarboxylových kyselín, ako kyseliny oxalovej alebo kyseliny vínnej alebo trikarboxylových kyselín, ako kyseliny citrónovej, na strane druhej, predovšetkým zmes kyseliny ortobóritej a kyseliny oxalovej, najlepšie spĺňa uvedené požiadavky. Každá zložka samotná katalyzuje reakciu iba nedostatočne. Až neočakávaný synergický účinok umožňuje optimálny výsledok.It has recently been found that a mixture of orthoboric acid on the one hand and certain dicarboxylic acids, such as oxalic acid or tartaric acid or tricarboxylic acids, such as citric acid, on the other hand, in particular a mixture of orthoboric acid and oxalic acid, best meets the above requirements. Each component alone catalyses the reaction insufficiently. The almost unexpected synergistic effect allows an optimal result.
Predmetom tohto vynálezu je tomu zodpovedajúci zlepšený spôsob výroby d,l-a-tokoferolu, prípadne d,Ι-α-tokoferylacetátu kyslo katalyzovanou reakciou 2,3,5-trimetylhydrochinónu s fytolom alebo izofytolom v rozpúšťadle pri zvýšenej teplote a prípadne nasledujúcou esterifikáciou získaného tokoferolu anhydridom kyseliny octovej, ktorý spočíva v tom, že sa reakcia uskutočňuje za prítomnosti zmesi kyseliny ortobóritej, na strane jednej a kyseliny oxalovej, kyseliny vínnej alebo kyseliny citrónovej, na strane druhej.The object of the present invention is a correspondingly improved process for the preparation of d, la-tocopherol or d, d-α-tocopheryl acetate by acid-catalyzed reaction of 2,3,5-trimethylhydroquinone with phytol or isophylene in a solvent at elevated temperature and optionally followed by esterification of the tocopherol obtained acetic acid, characterized in that the reaction is carried out in the presence of a mixture of orthoboric acid, on the one hand, and oxalic acid, tartaric acid or citric acid, on the other hand.
Výroba z 2,3,5-trimetylhydrochinónu a fytolu alebo izofytolu je známa a teda nepotrebuje, aby bola podrobne opísaná.The preparation of 2,3,5-trimethylhydroquinone and phytol or isophytol is known and therefore does not need to be described in detail.
Spôsob sa uskutoční predovšetkým výhodne, pokial sa ako katalyzátor použije kyselina oxalová alebo kyselina vínna, predovšetkým kyselina oxalová, v zmesi s kyselinou ortobóritou.The process is particularly advantageous when oxalic acid or tartaric acid, in particular oxalic acid, is used as a catalyst in admixture with orthoboric acid.
Kondenzácia 2,3,5-trimetylhydrochinónu s fytolom alebo izofytolom sa podlá tohto vynálezu uskutočňuje za prítomnosti približne od 0,2 do 7 % molárnych, s výhodou od 0,5 do 5 % molárnych kyseliny ortobóritej a od 0,4 do 14 % molárnych, s výhodou ' od 0 do 10 % molárnych kyseliny oxalovej, kyseliny vínnej alebo kyseliny citrónovej na mol 2,3,5-trimetylhydrochinónu. Kyselina ortobóritá a karboxylová kyselina sa s výhodou používajú približne v molárnom pomere 1:12.The condensation of 2,3,5-trimethylhydroquinone with phytol or isophytol according to the invention is carried out in the presence of from about 0.2 to 7 mol%, preferably from 0.5 to 5 mol%, of orthoboric acid and from 0.4 to 14 mol%. preferably from 0 to 10 mol% of oxalic acid, tartaric acid or citric acid per mole of 2,3,5-trimethylhydroquinone. The orthoboric acid and carboxylic acid are preferably used in a molar ratio of about 1:12.
Ako rozpúšťadlá pre reakciu sa s výhodou používajú alkylaromatické zlúčeniny, ako je toluén alebo xylén alebo ketóny, s teplotou varu približne od 70 do 140 °C. Predovšetkým výhodne sa pracuje v alifatických ketónoch, ako dietylketóne alebo metylizopropylketóne. Predovšetkým vhodné sú však také vysoko vriace rozpúšťadlá, ako je tetralín, pokial sa kondenzácia uskutočňuje pri silne zníženom tlaku.Alkyl aromatic compounds, such as toluene or xylene or ketones, with a boiling point of about 70 to 140 ° C are preferably used as solvents for the reaction. Particular preference is given to working in aliphatic ketones, such as diethyl ketone or methyl isopropyl ketone. However, highly boiling solvents such as tetraline are particularly suitable when condensation is carried out under strongly reduced pressure.
Reakčné teploty sú všeobecne približne od 70 až do 130 °C, s výhodou od 90 do 110 °C.Reaction temperatures are generally from about 70 to 130 ° C, preferably from 90 to 110 ° C.
Na uskutočnenie reakcie sa všeobecne postupuje tak, že sa do roztoku 2,3,5-trimetylhydrochinónu a katalytickej zmesi v rozpúšťadle, pri vysušovaní reakčnej zmesi s použitím vody a počas chladenia, i chladičom. Po skončení účinnou kvapalinovou : o sebe známym spôsobom, ketón po reakcii musí nahradiť rozpúšťadlom nemiešateľným s vodou, uhľovodíkom, aby sa mohol premyť získaný surový Pri použití alkylaromatických zlúčenín ako môže odpadnúť výmena rozpúšťadla. Avšak použitie že cirkulačného okruhu na odstraňovanie pridáva fytol alebo izofytol pod spätným reakcie (stanovuje sa vysoko chromatografiou) sa reakčná zmes spracuje Pri použití ketónov ako rozpúšťadla sa odstrániť a predovšetkým tokoferol. rozpúšťadiel alkylaromatických zlúčenín ako rozpúšťadiel má nevýhodu v tom, katalyzátor v malých množstvách z reakčnej zmesi vysublimuje.In order to carry out the reaction, it is generally carried out by adding a solution of 2,3,5-trimethylhydroquinone and a catalyst mixture in a solvent, drying the reaction mixture with water and cooling while cooling. Upon completion by an effective liquid: in a manner known per se, the ketone after the reaction must be replaced with a water-immiscible solvent, a hydrocarbon, so that the crude obtained can be washed using alkylaromatic compounds before solvent exchange can be dispensed with. However, using the recycle circuit to remove phytol or isophytol under reaction (as determined by high chromatography), the reaction mixture is worked up using ketones as solvent, and in particular tocopherol is removed. solvents of alkylaromatic compounds as solvents has the disadvantage that the catalyst sublimates from the reaction mixture in small amounts.
Premytie surového tokoferolu sa môže uskutočniť napr. zriedeným vodným roztokom hydroxidu sodného, zmesou metanolu a zriedenej vodnej kyseliny chlorovodíkovej a nakoniec zmesou metanolu a zriedeného vodného roztoku hydrogénuhličitanu sodného. Takto získaný tokoferol sa môže bud' izolovať ako taký alebo previesť na tokoferylacetát kyslo katalyzovanou reakciou s prebytkom anhydridu kyseliny octovej.The washing of the crude tocopherol can be carried out e.g. dilute aqueous sodium hydroxide solution, a mixture of methanol and dilute aqueous hydrochloric acid, and finally a mixture of methanol and dilute aqueous sodium bicarbonate. The tocopherol thus obtained can either be isolated as such or converted to tocopheryl acetate by an acid-catalyzed reaction with an excess of acetic anhydride.
Takto získaný tokoferylacetát sa môže čistiť frakcionovanou destiláciou pri silne zníženom tlaku.The tocopheryl acetate thus obtained can be purified by fractional distillation under strongly reduced pressure.
Spôsob sa môže kontinuálne.The process may be continuous.
Uskutočniť diskontinuálne, avšak tiežPerform discontinuously, but also
Pomocou spôsobu podlá tohto vynálezu sa môže získať d,1-a-tokoferol alebo jeho acetát jednoduchým spôsobom, ktorý je šetrný pre životné prostredie, vo veľmi dobrom výťažku a čistote.With the process of the present invention, d, l-α-tocopherol or its acetate can be obtained in a simple and environmentally friendly manner in very good yield and purity.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Príklad 1Example 1
Do banky s objemom 11 sa predloží 76 g (0,5 mol)To a flask of 11 was charged 76 g (0.5 mol)
2,3,5-trimetylhydrochinónu s 0,973 g (15,7 mmol) kyseliny ortobóritej a 2,83 g (31,4 mmol) kyseliny oxalovej v 200 g (245,2 ml) dietylketónu. Reakčná zmes sa počas sušenia pomocou cirkulačného okruhu na odstraňovanie vody počas 3 hodín uvedie do styku so 160 g (0,535 mol) izofytolu.2,3,5-trimethylhydroquinone with 0.973 g (15.7 mmol) of orthoboric acid and 2.83 g (31.4 mmol) of oxalic acid in 200 g (245.2 ml) of diethyl ketone. The reaction mixture was contacted with 160 g (0.535 mol) of isophytol during drying via a water removal circuit for 3 hours.
Po skončenom pridávaní izofytolu sa reakčná zmes varí ešte 30 minút pod spätným chladičom a potom sa nechá vychladnúť. Pomocou vysoko účinnej kvapalinovej chromátografie (100 % metanol, náplň Zorbax ODS 5 μπι, kolóna s rozmermi 4 mm x 25 mm, prietok 1 ml/min, ultrafialový detektor pri 220 nm) sa stanoví, že konverzia na 2,3,5-triemetylhydrochinón je väčšia ako 96 %.After completion of the addition of isophytol, the reaction mixture was refluxed for 30 minutes and then allowed to cool. High-performance liquid chromatography (100% methanol, Zorbax ODS 5 μπι, 4 mm x 25 mm column, flow rate 1 ml / min, ultraviolet detector at 220 nm) determined that conversion to 2,3,5-triethylhydroquinone is greater than 96%.
Nakoniec sa zo získaného roztoku zriedeným vodným roztokom hydroxiduFinally, from the solution obtained, dilute aqueous hydroxide solution
2,3,5-trimetylhydrochinón a katalyzátor tokoferolu extrahuje sodného nezreagovaný a potom sa roztok tokoferolu odfarbí vodným alkalickým roztokom síričitanu sodného.2,3,5-trimethylhydroquinone and the tocopherol catalyst are extracted with unreacted sodium and then the tocopherol solution is decolourised with an aqueous alkaline solution of sodium sulfite.
Potom sa dietylketón oddestiluje pri zníženom tlaku a zvyšný odparok sa uvedie do styku so 66 g (0,646 mol) anhydridu kyseliny octovej a 1,5 ml roztoku tvoreného 1 ml kyseliny sírovej v 100 ml anhydridu kyseliny octovej a (počas sledovania vysoko účinnou kvapalinovou chromatografiou) reakčná zmes sa zahrieva do varu pod spätným chladičom.Thereafter, the diethyl ketone was distilled off under reduced pressure, and the remaining residue was contacted with 66 g (0.646 mol) of acetic anhydride and 1.5 ml of a solution of 1 ml of sulfuric acid in 100 ml of acetic anhydride and (while monitoring by high performance liquid chromatography). the reaction mixture is heated to reflux.
Nakoniec sa zmes anhydridu kyseliny octovej a kyseliny octovej oddestiluje pri tlaku 2 kPa a ďalšou destiláciou pri zníženom tlaku sa získa 224 g čistého tokoferylacetátu. To zodpovedá výťažku 91,7 % teórie.Finally, the acetic anhydride / acetic acid mixture is distilled off at 2 kPa and further distillation under reduced pressure yields 224 g of pure tocopheryl acetate. This corresponds to a yield of 91.7% of theory.
Príklady 2 až 4Examples 2-4
Zmes pozostávajúca z 22,8 g (0,15 mmol) 2,3,5-trimetylhydrochinónu, 9,4 mmol karboxylovej kyseliny zrejmej z tabuľky a 0,293 g (4,7 mmol) kyseliny ortobóritej v 70 ml dietylketónu sa uvedie po kvapkách ,do styku so 48 g (0,16 mol) izofytolu, pri odstraňovaní vody cirkulačným okruhom, počas 90 minút intenzívneho chladenia pod spätným chladičom. Nakoniec sa reakčná zmes varí ešte 2 hodiny pod spätným chladičom. Počas reakcie sa pomocou okruhu odstránia približne 2 ml vody.A mixture of 22.8 g (0.15 mmol) of 2,3,5-trimethylhydroquinone, 9.4 mmol of the carboxylic acid shown in the table and 0.293 g (4.7 mmol) of orthoboric acid in 70 ml of diethyl ketone is added dropwise, Contact with 48 g (0.16 mol) of isophytol, while removing water through the circulating circuit, for 90 minutes of vigorous refluxing. Finally, the reaction mixture is refluxed for 2 hours. Approximately 2 mL of water was removed by the circuit during the reaction.
Nakoniec sa dietylketón oddestiluje pri zníženom tlaku (teplota kúpeľa 60 °C, vodná výveva, rotačná odparka), odparok sa vyberie 100 ml heptánu a heptánový roztok sa dvakrát premyje vždy 150 ml zmesi metanolu a 1-normálnej kyseliny chlorovodíkovej v pomere 1:1, potom jedenkrát zmesou 150 ml metanolu a 150 mlFinally, the diethyl ketone is distilled off under reduced pressure (bath temperature 60 ° C, water pump, rotary evaporator), the residue is taken up in 100 ml of heptane and the heptane solution is washed twice with 150 ml of a 1: 1 mixture of methanol and 1N hydrochloric acid. then once with a mixture of 150 ml of methanol and 150 ml
2,5 % vodného roztoku hydrogénuhličitanu sodného a nakoniec jedenkrát 75 ml zmesi metanolu a vody v pomere 1:1.Of a 2.5% aqueous solution of sodium bicarbonate and finally once with 75 ml of a 1: 1 mixture of methanol and water.
Odparením heptánu pri zníženom tlaku (teplota kúpeľa 70 °C, vodná výveva, rotačná odparka) sa získa surový tokoferol.Evaporation of heptane under reduced pressure (bath temperature 70 ° C, water pump, rotary evaporator) gave crude tocopherol.
Surový tokoferol sa acetyluje 19,2 g (0,19 mol) anhydridu kyseliny octovej za prítomnosti katalytického množstva kyseliny sírovej (pri teplote 142 až 145 °C počas 4 hodín) a reakčná zmes sa nakoniec odparí pri zníženom tlaku. Takto získaný surový tokoferylacetát sa podrobí frakcionalizovanej destilácii pri silne zníženom tlaku a výťažok sa stanoví plynovou chromatografiou. Získané výtažky d,Ι-α-tokoferylacetátu sú uvedené v nasledujúcej tabuľke.The crude tocopherol was acetylated with 19.2 g (0.19 mol) of acetic anhydride in the presence of a catalytic amount of sulfuric acid (at 142-145 ° C for 4 hours) and the reaction mixture was finally evaporated under reduced pressure. The crude tocopheryl acetate thus obtained is subjected to fractional distillation under strongly reduced pressure and the yield is determined by gas chromatography. The yields of d, Ι-α-tocopheryl acetate obtained are shown in the following table.
Tabuľkatable
Príklad Karboxylová kyselina Výťažok na d,Ι-α-tokoferylacetát (% teórie) kyselina oxalová kyselina L-(+)-vínna kyselina citrónováExample Carboxylic acid Yield on d, d-α-tocopheryl acetate (% of theory) oxalic acid L - (+) - tartaric citric acid
Príklad 5Example 5
a) Do miešacieho aparátu s objemom 500 ml, opatreného teplomerom, prikvapkávacou nálevkou a zariadením tvoriacim cirkulačný okruh na oddeľovanie vody, sa predloží zmes 150 ml toluénu, 22,8 g (0,15 mol)(a) A mixture of 150 ml of toluene, 22.8 g (0.15 mol) is charged to a 500 ml mixing apparatus equipped with a thermometer, a dropping funnel and a circulating water separating device.
2,3,5-trimetylhydrochinónu, 0,29 g (5 mmol) kyseliny ortobóritej a 0,85 g (10 mmol) kyseliny oxalovej. Táto zmes sa počas 1 hodiny uvedie do styku so 48 g (0,16 mol) izofytolu, počas intenzívneho chladenia pod spätným chladičom (približne na teplotu 100 °C pri tlaku 65 kPa) a odstraňovania vody pomocou cirkulačného okruhu a všetko sa potom ešte 1 hodinu nechá doreagovať. Pomocou okruhu sa oddelí približne 2,4 ml vody.2,3,5-trimethylhydroquinone, 0.29 g (5 mmol) of orthoboric acid and 0.85 g (10 mmol) of oxalic acid. This mixture was contacted with 48 g (0.16 mol) of isophytol for 1 hour, under vigorous reflux (approximately 100 ° C at 65 kPa), and the water was removed via a circulating circuit, and the mixture was stirred for 1 hour. let it react for one hour. Approximately 2.4 ml of water are separated by a circuit.
Nakoniec sa reakčná zmes ochladí na laboratórnu teplotu a trikrát premyje vždy 150 ml zmesi rovnakých dielov metanolu a 1-molárnej kyseliny chlorovodíkovej a potom dvakrát vždy 150 ml 50 % vodného metanolu a nakoniec odparí na rotačnej odparke (teplota kúpeľa 65 °C pri tlaku 3 kPa).Finally, the reaction mixture is cooled to room temperature and washed three times with 150 ml of a mixture of equal parts of methanol and 1 molar hydrochloric acid and then twice with 150 ml of 50% aqueous methanol each and finally evaporated on a rotary evaporator ( ).
Do získaného surového tokoferolu sa potom pridá 19,2 g (0,19 mol) anhydridu kyseliny octovej a stopa kyseliny sírovej. Zmes sa varí počas 4 hodín pod spätným chladičom a nakoniec sa odparí na rotačnej odparke (teplota kúpeľa 65 °C pri tlaku 3 kPa). Takto získaný surový tokoferylacetát sa podrobí frakcionovanej destilácii pri silne zníženom tlaku. Pri teplote 200 až 210 °C a tlaku 1 Pa prejde 65,2 g a-tokoferylacetátu, ktorý podlá analýzy plynovou chromatografiou (GC) má čistotu 98 %. To zodpovedá výťažku 90 % teórie.19.2 g (0.19 mol) of acetic anhydride and a trace of sulfuric acid are then added to the obtained crude tocopherol. The mixture was refluxed for 4 hours and finally evaporated on a rotary evaporator (bath temperature 65 ° C at 3 kPa). The crude tocopheryl acetate thus obtained is subjected to fractional distillation under strongly reduced pressure. 65.2 g of .alpha.-tocopheryl acetate are obtained at a temperature of 200 DEG-210 DEG C. and a pressure of 1 Pa, which, according to GC analysis, has a purity of 98%. This corresponds to a yield of 90% of theory.
Získaný výťažok sa môže v malom rozsahu zlepšiť zmenou spracovania reakčnej zmesi, pokial sa uskutoční ďalej popísaný variant spracovania b).The yield obtained can be improved to a small extent by changing the treatment of the reaction mixture, provided that the processing variant b) described below is carried out.
b) Reakčná zmes sa spracuje ako je popísané pod a), avšak po reakcii a nasledujúcej reakcii s izofytolom sa oddestiluje toluén (na rotačnej odparke pri teplote 65 °C a tlaku 3 kPa) a rozpúšťadlo sa nahradí rovnakým množstvom n-heptánu. Reakčná zmes sa premyje ako je popísané pod a) a potom sa n-heptán oddestiluje pri zníženom tlaku.b) The reaction mixture is worked up as described under a), but after the reaction and subsequent reaction with isophytol, toluene is distilled off (on a rotary evaporator at 65 ° C and 3 kPa) and the solvent is replaced with an equal amount of n-heptane. The reaction mixture is washed as described under a) and then n-heptane is distilled off under reduced pressure.
α-Tokoferylacetát získaný frakcionovanou destiláciou má podlá plynovej chromatografie čistotu 98 %. Výťažok zodpovedá 92 % teórie.The α-tocopheryl acetate obtained by fractional distillation has a purity of 98% according to gas chromatography. Yield: 92%.
Príklad 6Example 6
Do miešacieho aparátu s objemom 500 ml, opatreného teplomerom a prikvapkávacou nálevkou, sa predloží zmes 150 ml tetralínu, 22,8 g 2,3,5-trimetylhydrochinónu, 0,29 g kyseliny ortobóritej a 0,85 g kyseliny oxalovej. Táto zmes sa počas 1 hodiny uvedie do styku so 48 g izofytolu, počas intenzívneho chladenia pod spätným chladičom (približne na teplotu 95 až 100 °C pri tlaku 8 kPa) a všetko sa potom ešte jednu hodinu nechá doreagovať. Reakčná voda sa počas reakcie odvádza vo forme pary cez vyhrievaný mostík a kondenzuje v chladenej predlohe (zachytí sa približne 2,6 g vody). Pritom sa tiež pridá malý podiel katalyzátora.A mixture of 150 ml of tetraline, 22.8 g of 2,3,5-trimethylhydroquinone, 0.29 g of orthoboric acid and 0.85 g of oxalic acid is introduced into a 500 ml mixing apparatus equipped with a thermometer and an addition funnel. This mixture is contacted with 48 g of isophytol for 1 hour, under vigorous reflux (approximately 95-100 ° C at 8 kPa), and then left to react for one hour. The reaction water is removed as a steam through a heated bridge during the reaction and condensed in a chilled flask (approximately 2.6 g of water is collected). A small proportion of the catalyst is also added.
Nakoniec sa reakčná zmes ochladí na teplotu 40 °C, pridá sa 100 ml heptánu a vzniknutá zmes sa premyje trikrát vždy 150 ml roztoku rovnakých dielov metanolu a 1-molárnej vodnej kyseliny chlorovodíkovej a potom dvakrát vždy 100 ml 50 % vodného metanolu. Organická fáza sa zbaví v tejto chvíli odparením heptánu na rotačnej odparke (teplota kúpeľa 65 °C pri tlaku 3 kPa) a tetralín sa oddestiluje cez mostík (pri teplote 50 °C a tlaku približne 50 Pa).Finally, the reaction mixture is cooled to 40 [deg.] C., 100 ml of heptane are added and the mixture is washed three times with 150 ml of a solution of equal parts of methanol and 1 molar aqueous hydrochloric acid and then twice with 100 ml of 50% aqueous methanol each. At this point, the organic phase is freed by rotary evaporation of heptane (bath temperature 65 ° C at 3 kPa) and the tetralin is distilled off over a bridge (at 50 ° C and about 50 Pa).
Do odparku sa pridá 19,2 g anhydridu kyseliny octovej a stopa kyseliny sírovej. Vzniknutá zmes sa zahrieva počas 4 hodín na teplotu spätného toku a potom sa odparí na rotačnej odparke (teplota kúpeľa 65 °C pri tlaku 3 kPa a nakoniec 500 Pa). Destilácia pri silne zníženom tlaku cez mostík pri teplote 204 až 210 °C a tlaku 2 Pa poskytne 68,6 g α-tokoferylacetátu, ktorý podľa analýzy plynovou chromatografiou (GC) má čistotu 92 %. To zodpovedá výťažku 89 % teórie.19.2 g of acetic anhydride and a trace of sulfuric acid are added to the residue. The resulting mixture was heated to reflux for 4 hours and then evaporated on a rotary evaporator (bath temperature 65 ° C at 3 kPa and finally 500 Pa). Distillation under high vacuum over a bridge at 204 to 210 ° C and 2 Pa gives 68.6 g of α-tocopheryl acetate, which is 92% pure by gas chromatography (GC) analysis. This corresponds to a yield of 89% of theory.
TV ŕf/to-fyTV-to-fy
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CZ (1) | CZ281829B6 (en) |
DE (2) | DE4208477A1 (en) |
ES (1) | ES2101306T3 (en) |
HU (1) | HU214095B (en) |
SK (1) | SK112094A3 (en) |
WO (1) | WO1993019057A1 (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3416281B2 (en) * | 1994-04-12 | 2003-06-16 | エーザイ株式会社 | Method for producing α-tocopherol derivative and catalyst |
US5663376A (en) † | 1994-07-27 | 1997-09-02 | Eisai Co., Ltd. | Process for the preparation of α-tocopherol |
DE19524928A1 (en) * | 1995-07-08 | 1997-01-09 | Basf Ag | Process for the rectification of mixtures of high-boiling air and / or temperature sensitive substances, which require a high separation performance, in a fine vacuum, as well as columns suitable for this process |
US5886196A (en) * | 1996-01-12 | 1999-03-23 | Roche Vitamins Inc. | Method of catalyzing condensation reactions |
DE10011403A1 (en) * | 2000-03-09 | 2001-09-13 | Degussa | Production of alpha-tocopherol acetate useful as feed additive involves condensation of trimethylhydroquinone and isophytol in presence of a regenerable catalyst system followed by acylation of the resultant alpha-tocopherol |
ATE298330T1 (en) | 2000-11-22 | 2005-07-15 | Basf Ag | METHOD FOR THE CONTINUOUS ACYLATION OF CHROMANOLESTER DERIVATIVES |
DE10135714A1 (en) * | 2001-07-21 | 2003-02-06 | Basf Ag | Processing of vitamin E-acetate containing product stream, comprises use of thin film evaporator, falling film evaporator or flash evaporator with at least two step partial condensation |
US8183396B2 (en) | 2004-08-19 | 2012-05-22 | Dsm Ip Assets B.V. | Process for the working-up of a vitamin E- and vitamin E-acetate- containing mixture or products stream |
ATE502931T1 (en) | 2004-08-19 | 2011-04-15 | Dsm Ip Assets Bv | METHOD FOR RECTIFICATION OF VITAMIN E ACETATE |
DE102005013103A1 (en) | 2005-03-18 | 2006-09-28 | Sms Demag Ag | Controlled thickness reduction in hot-dip coated hot rolled steel strip and equipment used in this case |
CN106478581A (en) * | 2016-08-30 | 2017-03-08 | 芜湖华海生物工程有限公司 | A kind of preparation method of Vitwas E |
CN113083339B (en) * | 2021-04-15 | 2022-11-08 | 万华化学(四川)有限公司 | Catalyst for preparing vitamin E and preparation method and application thereof |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3459773A (en) * | 1966-12-27 | 1969-08-05 | Takasago Perfumery Co Ltd | Process for producing alpha-tocopherol and its esters |
US3708505A (en) * | 1971-02-25 | 1973-01-02 | Diamond Shamrock Corp | Process for preparation of d,l-alpha tocopherol |
BE810299A (en) * | 1974-01-29 | 1974-05-16 | METHOD OF MANUFACTURING COMPOUNDS CONTAINING A CHROMAN CORE. | |
JPS6019309B2 (en) * | 1976-09-29 | 1985-05-15 | 日清製粉株式会社 | Production method of high purity dl-α-tocopherol |
US4217285A (en) * | 1976-09-29 | 1980-08-12 | Nisshin Flour Milling Co., Ltd. | Process for the preparation of Dl-α-tocopherol of high purity |
DE3367100D1 (en) * | 1982-07-29 | 1986-11-27 | Basf Wyandotte Corp | Alpha tocopherol process |
-
1992
- 1992-03-17 DE DE4208477A patent/DE4208477A1/en not_active Withdrawn
-
1993
- 1993-03-05 DE DE59306604T patent/DE59306604D1/en not_active Expired - Fee Related
- 1993-03-05 WO PCT/EP1993/000498 patent/WO1993019057A1/en active IP Right Grant
- 1993-03-05 HU HU9402669A patent/HU214095B/en not_active IP Right Cessation
- 1993-03-05 CZ CZ942250A patent/CZ281829B6/en not_active IP Right Cessation
- 1993-03-05 EP EP93906485A patent/EP0631577B1/en not_active Expired - Lifetime
- 1993-03-05 SK SK1120-94A patent/SK112094A3/en unknown
- 1993-03-05 ES ES93906485T patent/ES2101306T3/en not_active Expired - Lifetime
- 1993-03-05 JP JP5516203A patent/JP2550288B2/en not_active Expired - Lifetime
- 1993-03-05 US US08/302,743 patent/US5468883A/en not_active Expired - Fee Related
- 1993-03-16 CA CA002091729A patent/CA2091729C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
ES2101306T3 (en) | 1997-07-01 |
CA2091729A1 (en) | 1993-09-18 |
JP2550288B2 (en) | 1996-11-06 |
CZ281829B6 (en) | 1997-02-12 |
DE4208477A1 (en) | 1993-09-23 |
US5468883A (en) | 1995-11-21 |
DE59306604D1 (en) | 1997-07-03 |
EP0631577B1 (en) | 1997-05-28 |
CA2091729C (en) | 1999-11-23 |
WO1993019057A1 (en) | 1993-09-30 |
HU9402669D0 (en) | 1995-02-28 |
HUT71257A (en) | 1995-11-28 |
EP0631577A1 (en) | 1995-01-04 |
HU214095B (en) | 1998-03-02 |
JPH07507274A (en) | 1995-08-10 |
CZ225094A3 (en) | 1995-04-12 |
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